Configure carbon production, process-gas treatment, boiler duty and the customer steam load as a connected system.
Turn stable carbonization heat into useful industrial steam.
A steam project should be designed around the receiving process load. Carbonization gas, supplementary fuel, boiler duty, water treatment and backup capacity must work as one operating system.
Keep carbon quality and steam reliability under separate control
The carbonizer creates the primary product; the energy train converts suitable process gas and heat into a controlled utility.
- 01Biomass drying and feeding
- 02Continuous carbonization
- 03Dust and condensable separation
- 04Gas cleaning and controlled combustion
- 05Steam generation and water treatment
- 06Distribution, metering and backup supply
Define the user before defining the boiler
Food and chemical plants require a clear hourly steam profile, pressure, quality and continuity basis.
Steam demand
Provide minimum, normal and peak demand, operating hours, pressure, temperature and seasonal production schedule.
Water system
Define raw-water quality, treatment, deaeration, blowdown, condensate return and make-up-water capacity.
Fuel stability
Gas cleaning, buffer volume, burner turndown and supplementary fuel determine pressure stability during feed or quality changes.
Interface boundary
Agree the battery limit for boiler house, steam header, midimentu, condensate return, civil works and operating responsibility.
Verify both carbon output and usable steam
Acceptance should be based on documented feedstock, operating conditions and measurement methods.
Carbon product
Record yield and product properties only against the tested biomass and agreed thermal program.
Steam output
Meter flow, pressure and temperature during a defined stable operating window instead of using theoretical heat alone.
Emissions boundary
Identify combustion, particulate and condensable controls and the local monitoring or permit requirements.
Continuity plan
Define startup, shutdown, maintenance, low-gas operation and backup-steam behavior for the receiving plant.
See the connected equipment boundary.
Reference visuals support early layout discussion. Final equipment, arrangement and interfaces are confirmed from the project material and site.
Tradusí echonan di proyekto den un lista di ekipo.
E matris di referensia aki ta mustra e lógika di desishon. Kantidatnan final, modelonan i interfasenan ta pertenesé na e proposishon di proyekto aprobá.
| Blòki di sistema | Alkanse típiko | Base di konfigurashon |
|---|---|---|
| Gas preparation | Stòf, condensable and moisture control with safe buffering | Carbonization-gas variability and burner limits |
| Combustion system | Controlled burner, combustion chamber and safety interlocks | Steam duty, turndown and supplementary-fuel plan |
| Boiler island | Boiler, economizer, blowdown, instruments and protection | Pressure, temperature and operating code basis |
| Water and condensate | Treatment, deaeration, make-up water and condensate return | Source-water quality and user return conditions |
| Steam delivery | Header, midimentu, pressure control and backup interface | Minimum, normal and peak customer demand |
Adelantá e proyekto solamente ora e evidensia nesesario ta disponibel.
Kada porta ta kombertí informashon di kliente den un output tékniko òf komersial definí pa e siguiente desishon.
Load profile
Capture minimum, normal and peak demand plus continuity requirements.
SalidaMetered or documented steam-demand basisBalansa di energia
Match process-gas availability, internal heat demand and backup fuel.
SalidaVerified preliminary heat balanceUtility design
Define boiler, awa, condensate, header and emissions interfaces.
SalidaConnected utility configurationAcceptance plan
Agree test feedstock, stable window, meters and backup behavior.
SalidaMeasurable project acceptance sheetPreguntanan pa resolvé promé ku konfigurashon.
Kontesta ta definí e frontera di ingenieria; nan no ta remplasá prueba di material representativo òf revishon di kumplimentu lokal.
What information is needed from the steam user?
Provide minimum, normal and peak steam demand, pressure, temperature, skema di operashon, condensate return, water quality and continuity requirement.
Can process gas alone guarantee continuous steam supply?
Not without verification. Buffering, burner turndown, supplementary fuel and backup capacity may be needed when feedstock or gas production varies.
What belongs in the steam-system boundary?
The scope may include gas treatment, combustion, boiler, water treatment, deaeration, blowdown, steam header, midimentu, condensate return and backup interfaces.
How should steam acceptance be measured?
Use metered flow, pressure and temperature during a defined stable operating window with the agreed biomass, carbonization conditions and auxiliary loads.
Definí e material promé ku selektá e ekipo.
Kompartí un deskripshon di material representativo, volúmen disponibel, status di e sitio i salidanan di meta. YUSHUNXIN lo usa e echonan ei pa prepará e frontera di proseso relevante i e diskushon di konfigurashon.
Carbonization with waste-heat steam supply
Configure the carbonization line and receiving steam load from one measured heat and mass balance.
Material ku ta drenta
Prepared biomass plus hourly/daily feed profile and target carbon specification.
Resultadonan ferwagt
Biochar and a qualified waste-heat stream for an agreed steam duty.
Interfasnan di proyekto
Feed drying, carbonization gas, combustion, waste-heat boiler, water treatment, steam pressure/load and operating control.
Usa solamente e fila ku ta kuadra ku e frontera di e proseso selektá.
| Referensia di katalogo | Kapasidat | Poder | Envelop físiko | Frontera inkluí |
|---|---|---|---|---|
| SXTD820Continuous carbonization | 1–2 m³/h | 95 kW | 600 m² catalogue land reference | Prepared biomass continuous carbonization line |
| SXTD1200Continuous carbonization | 3–5 m³/h | 110 kW | 650 m² catalogue land reference | Prepared biomass continuous carbonization line |
| SXTD1500Continuous carbonization | 5–8 m³/h | 153 kW | 800 m² catalogue land reference | Prepared biomass continuous carbonization line |
| SXTD1800Continuous carbonization | 8–10 m³/h | 178 kW | 800 m² catalogue land reference | Prepared biomass continuous carbonization line |
| SXTD2000 - 10–14 classContinuous carbonization | 10–14 m³/h | 190 kW | 850 m² catalogue land reference | Catalogue prints SXTD2000 for this class |
| SXTD2000 - 14–17 classContinuous carbonization | 14–17 m³/h | 220 kW | 850 m² catalogue land reference | Catalogue repeats SXTD2000; final model code requires written confirmation |
Regla di konfigurashon: kapasidat di katalogo ta un referensia di planifikashon. Produkshon stabil, energia instalá/operashonal, pegada, rekuperashon, puresa, emishon i demanda di utilidat ta rekerí e lista di ekipo aprobá, material representativo i kondishonnan di aseptashon por eskrito.
Informashon nesesario promé ku konfigurashon i sitashon
- Potrètnan di material representativo, spesifikashonnan i muestra disponibel.
- Kapasidat nesesario mas oranan pa turno, turno pa dia i dianan di operashon.
- Outputnan di meta, método di muestra i rekisitonan di risibí di awa abou.
- Pais di e sitio, poder disponibel, kombustibel, awa, aire komprimí i límitenan di edifisio.
- Medioambiente lokal, kandela, rekisitonan di almasenamentu i seguridat na trabou.
- Frontera di entrega pidi: ekipo, diseño, instalashon, enkargo i entrenamentu.
